1. Catalytic oxidation of calcium bisulfite in the wet limestone–gypsum flue gas desulfurization process
- Author
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Marco Tammaro, Marina Prisciandaro, Amedeo Lancia, Dino Musmarra, Lancia, A., Musmarra, Dino, Prisciandaro, M., Tammaro, M., Lancia, Amedeo, D., Musmarra, M., Prisciandaro, and M., Tammaro
- Subjects
Flue gas ,Calcium bisulfite ,Applied Mathematics ,General Chemical Engineering ,Inorganic chemistry ,General Chemistry ,Partial pressure ,Industrial and Manufacturing Engineering ,Flue-gas desulfurization ,Reaction rate ,chemistry.chemical_compound ,Catalytic oxidation ,chemistry ,Calcium sulfite ,Reaction regime ,Oxidation ,Desulfurization ,Manganous sulfate ,Dissolution - Abstract
A study on the oxidation of calcium sulfite catalyzed by Mn(2+) is presented in this paper. A laboratory-scale well-mixed thermostated reactor was used, with continuous feeding of both gas and liquid phase. The gas phase was a mixture of oxygen and nitrogen, with O(2) partial pressure varying from 5.1 to 40.5 kPa. The liquid phase was obtained by mixing inside the reactor two separate aqueous solutions, one obtained by dissolving Ca(OH)(2) into a SO(2) solution, and the other one containing manganous sulfate. The temperature was kept constant in all the experiments at 45 degrees C. The results show that increasing catalyst concentration, the transition takes place from slow kinetic to slow diffusional and eventually to fast reaction regime. (C) 1999 Elsevier Science Ltd. All rights reserved.
- Published
- 1999